EP0863884B1 - Process for preparing bis-alkoxy-triazinyl-amino-containing stilbene disulphonic acids or their derivatives - Google Patents

Process for preparing bis-alkoxy-triazinyl-amino-containing stilbene disulphonic acids or their derivatives Download PDF

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EP0863884B1
EP0863884B1 EP96939062A EP96939062A EP0863884B1 EP 0863884 B1 EP0863884 B1 EP 0863884B1 EP 96939062 A EP96939062 A EP 96939062A EP 96939062 A EP96939062 A EP 96939062A EP 0863884 B1 EP0863884 B1 EP 0863884B1
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Prior art keywords
amino
stilbene
triazinyl
derivatives
water
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German (de)
French (fr)
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EP0863884A2 (en
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Ulrich Feldhues
Uwe Vogt
Udo Eckstein
Rolf Brockmann
Dietmar Fiedel
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Bayer AG
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Bayer AG
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    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07DHETEROCYCLIC COMPOUNDS
    • C07D251/00Heterocyclic compounds containing 1,3,5-triazine rings
    • C07D251/02Heterocyclic compounds containing 1,3,5-triazine rings not condensed with other rings
    • C07D251/12Heterocyclic compounds containing 1,3,5-triazine rings not condensed with other rings having three double bonds between ring members or between ring members and non-ring members
    • C07D251/26Heterocyclic compounds containing 1,3,5-triazine rings not condensed with other rings having three double bonds between ring members or between ring members and non-ring members with only hetero atoms directly attached to ring carbon atoms
    • C07D251/40Nitrogen atoms
    • C07D251/48Two nitrogen atoms
    • C07D251/52Two nitrogen atoms with an oxygen or sulfur atom attached to the third ring carbon atom
    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21HPULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
    • D21H21/00Non-fibrous material added to the pulp, characterised by its function, form or properties; Paper-impregnating or coating material, characterised by its function, form or properties
    • D21H21/14Non-fibrous material added to the pulp, characterised by its function, form or properties; Paper-impregnating or coating material, characterised by its function, form or properties characterised by function or properties in or on the paper
    • D21H21/30Luminescent or fluorescent substances, e.g. for optical bleaching

Definitions

  • the invention relates to a process for the preparation of bis-alkoxy-triazinyl-amino-containing Stilbene disulfonic acids or their derivatives and their use as optical Brightener for organic material, especially for paper and cellulose, in particular for photo paper.
  • Optical brighteners based on substituted bis-triazinylamino-stilbene-2,2'-disulfonic acids, where each triazine residue in addition to the substitution by the flavonic acid and another amine is substituted with an alkoxy group, and a process for their production is known in large numbers.
  • the alkoxy radical is normally only present in the first or in the second stage of an acid binding agent. So you put an alkanol with cyanuric chloride or with a cyanuric chloride derivative containing two chlorine atoms around. Considerable undesirable side reactions occur due to multiple reactions on the cyanuric chloride.
  • the introduction of an alkoxy group in the third stage, i.e. in a cyanuric chloride derivative containing only one chlorine atom requires special conditions, such as. working in anhydrous glycols or glycol monoalkyl ethers in the presence of the corresponding sodium alcoholate (DE-A 1 444 015).
  • JP-A 305 983 describes bis-triazinylamino-stilbene-2,2'-disulfonic acid derivatives Methanol reacted in a 1: 2 ratio or with a small excess of methanol.
  • DE-A-2 335 570 describes that when using glycols or glycol monoalkyl ethers it is possible to react them with bis-triazinylamino-stilbene-2,2'-disulfonic acid derivatives in the third stage, ie with a Cyanuric chloride derivative that only has one chlorine atom on each triazine ring.
  • the yield of this procedure is only between 50 and 80% and therefore makes the procedure unattractive.
  • a process has now been found for producing bis-alkoxy-triazinyl-amino-containing stilbene disulfonic acids or their derivatives, in which bis-chloro-triazinyl-amino-containing stilbene disulfonic acids are reacted with a C 1 -C 4 -monoalkanol, characterized in that that at least 10 moles of C 1 -C 4 -monoalkanol are used per 1 mole of bis-chloro-triazinyl-amino-containing stilbene-disulfonic acid or its derivatives and the C 1 -C 4 -monoalkanol is used together with water, the water content of the reaction mixture preferably 10-80% by weight, preferably 25-60% by weight, based on the reaction mixture.
  • At least 20 moles of the C 1 -C 4 -monoalkanol are used for 1 mole of a bis-chloro-triazinyl-amino-containing stilbene disulfonic acid or its derivatives.
  • 50-500 moles, in particular 100-300 moles of C 1 -C 4 -monoalkanol per mole of the bis-chloro-triazinyl-amino-containing stilbene sulfonic acid compound are particularly preferably used.
  • the preferred C 1 -C 4 monoalkanols are methanol, ethanol, isopropanol, n-propanol, n-butanol, sec-butanol or tert-butanol, in particular methanol
  • the process according to the invention is preferably carried out in the presence of an acid-binding Carried out, preferably as the acid-binding agent Alkali hydroxide, especially potassium or sodium hydroxide is used.
  • the Acid-binding agent is preferably used in an amount of 2 to 6 mol equivalents per mole of the bis-chloro-triazinyl-amino-containing stilbene disulfonic acid or its Derivatives used, preferably in an amount of 3 to 4 mol equivalents.
  • inventive method in which the compounds of Formula (II) can not be isolated between their preparation.
  • the compound of formula (II) in the form of its aqueous reaction solution, if necessary after concentration and if necessary (partial) desalination to use in the manufacturing process according to the invention.
  • the compounds of the formula (I) are obtained starting from a compound of the formula (II) in which R 3 and R 4 independently of one another are NR 5 R 6 , where R 5 is hydrogen or optionally substituted C 1 -C 6 alkyl and R 6 can have the meanings given under R 5 or optionally substituted C 5 -C 8 cycloalkyl or optionally substituted C 6 -C 10 aryl, or NR 5 R 6 for optionally by C 1 -C 4 alkyl, in particular methyl-substituted morpholino, piperidino or hexamethyleneimino
  • Preferred substituents of the C 1 -C 6 -alkyl radical in the meaning of R 5 and R 6 are, for example, hydroxyl, C 1 -C 6 -alkoxy, C 2 -C 8 -alkoxy-substituted C 2 -C 8 -alkoxy, C 1 -C 6 alkylamino or C 1 -C 6 dialkylamino, cyano or sulfonic acid or sulfonate.
  • C 5 -C 8 cycloalkyl are: halogen, in particular fluorine, chlorine and bromine, C 1 -C 6 alkyl, C 1 -C 6 alkoxy, sulfamoyl or sulfonyl, in particular C 1 -C 4 - Alkyl.
  • Sulfo-substituted phenyl is particularly suitable as an optionally substituted C 6 -C 10 aryl.
  • R 5 very particularly preferably represents hydrogen, methyl, sulfoethyl or its alkali salt or hydroxyethyl and R 6 represents sulfoethyl or its alkali salt, hydroxyethyl or disulfo-substituted phenyl.
  • radicals R 3 , R 4 and R 1 and R 2 are identical.
  • the radical M which is preferably hydrogen or an alkali metal such as sodium, Potassium or lithium does not have to be on every sulfonic acid group in the molecule be identical.
  • reaction mixture obtainable by the process according to the invention to a pH of less than 10, preferably less than 8, and to remove the excess C 1 -C 4 -monoalkanol, preferably by distillation.
  • Preferred compounds of the formula (IV) are those in which the SO 3 M groups of the terminal benzene ring are in the 2- and 5-positions.
  • the compounds of formula (IV) can be analogous to the procedure described above getting produced.
  • the compounds (I) prepared by the process according to the invention and the new compounds of the formula (IV) are outstandingly suitable as optical brighteners for organic materials, preferably for cellulose, polyamide, wool, silk and Paper, in particular for photographic paper. They can also be added to detergents.
  • the compounds of formula (I) can e.g. incorporated in bulk or on the Surface of the materials to be lightened are applied. Particularly preferred The amounts used are 0.0001 to 2% by weight, based on the material to be lightened.
  • the pH is adjusted to 6.5 to 7.0 in about 1 hour by adding 10% hydrochloric acid.
  • methanol or methanol-water is distilled off until a constant boiling point of 100 ° C. is reached.
  • the mixture is made up to 1500ml with water at approx. 30 ° C.
  • the solution is then suctioned off first through a blue-band filter and then through a 0.8 ⁇ m filter in order to free the solution from all turbidity and suspended matter which impede the permeate flow.
  • the 1500 ml are filled into a pressure permeation system.
  • the first 500 ml of permeate are removed at 40 to 50 ° C and approx. 40 bar.
  • 500 ml of water are added and the second approx. 500 ml of permeate are removed.
  • 500 ml of water are added and the third approximately 500 ml of permeate are removed.
  • 500 ml of water are added and the fourth approximately 500 ml of permeate are removed.
  • the concentrate is evaporated to dryness in a crystallizing dish in a vacuum drying cabinet (50 ° C.) and comminuted in a friction dish.
  • the product contains less than 2% NaCl and approx. 1% H 2 O, so that the theoretical yield is approx. 94%.
  • the pH is adjusted to 6.5 to 7.0 in about 1 hour by adding 10% hydrochloric acid.
  • methanol or methanol-water is distilled off until a constant boiling point of 100 ° C. is reached. is.
  • the mixture is made up to 1,800 ml with water at approx. 40 to 50 ° C.
  • the solution is then suctioned off first through a blue band filter and then through a 0.8 ⁇ m filter in order to remove all turbidity and suspended matter which impede the permeate flow to free.
  • the 1,800 ml are filled in a pressure permeation system at 40 to 50 ° C and approx. 40 bar, the first 600 ml permeate are removed.
  • 600 ml of water are added and the second approximately 600 ml of permeate are removed.
  • 600 ml of water are added and the third approximately 600 ml of permeate are removed.
  • 600 ml of water are added and the fourth approximately 600 ml of permeate are removed.
  • the concentrate is evaporated to dryness in a crystallizing dish in a vacuum drying cabinet (50 ° C.) and comminuted in a friction dish. Yield: 140 g of light yellow powder.
  • the product contains less than 1% NaCl and less than 1% water, so that the theoretical yield is 95%
  • the pH is adjusted to 6.5 to 7.0 in about 1 hour by adding 10% hydrochloric acid.
  • methanol or methanol-water is distilled off until a constant boiling point of 100 ° C. is reached.
  • the batch is made up to 1200 ml with water at approx. 50 ° C.
  • the solution is then suctioned off first through a blue-band filter and then through a 0.8 ⁇ m filter in order to free the solution from all turbidity and suspended matter which impede the permeate flow.
  • the 1,200 ml are filled into a pressure permeation system.
  • the first 400 ml of permeate are removed at approx. 50 ° C and approx. 40 bar.
  • the product contains less than 1% NaCl and less than 1% water, so that the theoretical yield is 95%.
  • the temperature is set to 45 ° C
  • a solution of 167 g of 4,4'-bis [(4- (2,5-disulfo) anilino-6-chloro-1,3,5-triazine) at about 45 ° C. is then heated at 45 ° C. within 1 hour.
  • 2-yl) amino] -stilbene-2,2'-disulfonic acid hexasodium salt dropped in 1 275 ml of water. The temperature is kept for 4 hours.
  • the pH is adjusted to 6.5 to 7.0 in about 1 hour by adding 10% hydrochloric acid. Thereafter, ethanol or ethanol-water is distilled off until a constant boiling point of 100 ° C. is reached.
  • the mixture is made up to 1500 ml with water at approx. 50 ° C.
  • the solution is then suctioned off first through a blue-band filter and then through a 0.8 ⁇ m filter in order to free the solution from all turbidity and suspended matter which impede the permeate flow.
  • the 1,500 ml are filled into a pressure permeation system. The first 500 ml of permeate are removed at 40 to 50 ° C and approx. 40 bar. 500 ml of water are added and the second approx. 500 ml of permeate are removed.
  • the product contains less than 2% NaCl and less than 2% water, so that the theoretical yield is 93%.
  • the solution is then suctioned off first through a blue-band filter and then through a 0.8 ⁇ m filter in order to free the solution from all turbidity and suspended matter which impede the permeate flow.
  • the 500ml are filled in a pressure permeation system.
  • the first 150 ml of permeate are removed at 40 - 50 ° C and approx. 40 bar.
  • 150 ml of water are added and the second approximately 150 ml of permeate are removed.
  • 150 ml of water are added and the third approximately 150 ml of permeate are removed.
  • 150 ml of water are added and the fourth approximately 150 ml of permeate are removed.
  • the concentrate is evaporated to dryness in a crystallizing dish in a vacuum drying cabinet (50 ° C.) and comminuted in a friction dish. Yield: 56 g of yellow powder 4,4'-bis [(2- (4-sulfo) anilino-6-methoxy-1,3,5-triazin-2-yl) amino] -stilbene-2,2'-disulfonic acid tetrasodium salt
  • the product still contains 1% NaCl and 2% water, so that there is a yield the theory of 92%.

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Plural Heterocyclic Compounds (AREA)
  • Treatments For Attaching Organic Compounds To Fibrous Goods (AREA)
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Abstract

The invention concerns a process for preparing bis-alkoxy-triazinyl-amino-containing stilbene disulphonic acids or their derivatives, characterized in that bis-chlorotriazinyl-amino-containing stilbene disulphonic acids or their derivatives are reacted with at least 10 mol equivalents of a C1-C4 monoalkanol, relative to the stilbene disulphonic acid compound.

Description

Die Erfindung betrifft ein Verfahren zur Herstellung von bis-alkoxy-triazinyl- aminohaltigen Stilben-disulfonsäuren oder deren Derivaten und ihre Verwendung als optische Aufheller für organisches Material, vornehmlich für Papier und Cellulose, insbesondere für Photopapier.The invention relates to a process for the preparation of bis-alkoxy-triazinyl-amino-containing Stilbene disulfonic acids or their derivatives and their use as optical Brightener for organic material, especially for paper and cellulose, in particular for photo paper.

Optische Aufheller auf Basis substituierter bis-triazinylamino-stilben-2,2'-disulfonsäuren, bei denen jeweils jeder Triazinrest neben der Substitution durch die Flavonsäure und ein weiteres Amin mit einem Alkoxyrest substituiert ist, und ein Verfahren zur ihrer Herstellung sind in großer Zahl bekannt.Optical brighteners based on substituted bis-triazinylamino-stilbene-2,2'-disulfonic acids, where each triazine residue in addition to the substitution by the flavonic acid and another amine is substituted with an alkoxy group, and a process for their production is known in large numbers.

Der Alkoxyrest wird normalerweise nur in der ersten bzw. in der zweiten Stufe in Gegenwart eines säurebindenden Mittels eingeführt. Man setzt also ein Alkanol mit Cyanurchlorid oder mit einem noch zwei Chloratome enthaltenden Cyanurchloridderivat um. Dabei treten erhebliche unerwünschte Nebenreaktionen durch Mehrfachumsetzung am Cyanurchlorid auf. Das Einführen einer Alkoxygruppe in der dritten Stufe, d.h. in ein nur noch ein Chloratom enthaltendes Cyanurchloridderivat, erfordert spezielle Bedingungen, wie z.B. das Arbeiten in wasserfreien Glykolen bzw. Glykolmonoalkylethern in Gegenwart des entsprechenden Natriumalkoholats (DE-A 1 444 015).The alkoxy radical is normally only present in the first or in the second stage of an acid binding agent. So you put an alkanol with cyanuric chloride or with a cyanuric chloride derivative containing two chlorine atoms around. Considerable undesirable side reactions occur due to multiple reactions on the cyanuric chloride. The introduction of an alkoxy group in the third stage, i.e. in a cyanuric chloride derivative containing only one chlorine atom requires special conditions, such as. working in anhydrous glycols or glycol monoalkyl ethers in the presence of the corresponding sodium alcoholate (DE-A 1 444 015).

In JP-A 305 983 werden Bis-triazinylamino-stilben-2,2'-disulfonsäurederivate mit Methanol im Verhältnis 1:2 bzw. mit geringem Methanolüberschuß umgesetzt.JP-A 305 983 describes bis-triazinylamino-stilbene-2,2'-disulfonic acid derivatives Methanol reacted in a 1: 2 ratio or with a small excess of methanol.

In DE-A-2 335 570 wird beschrieben, daß es bei der Verwendung von Glykolen bzw. Glykolmonoalkylethern möglich ist, diese mit Bis-triazinylamino-stilben-2,2'-disulfonsäurederivaten in der dritten Stufe zur Reaktion zu bringen, d.h. mit einem Cyanurchloridderivat, das nur noch ein Chloratom an jedem Triazinring trägt. Die Ausbeute dieser Verfahrensweise beträgt jedoch nur zwischen 50 und 80 % und macht das Verfahren daher unattraktiv. Es bestand somit ein Bedürfnis, nach einem Verfahren mit dem man selektiv und mit verbesserten Ausbeuten, ohne den Einsatz aufwendiger und teuerer Reagenzien exakt einen C1-C4-Alkoxyrest pro Cyanurchlorideinheit in die Bis-triazinylamino-stilben-2,2'-disulfonsäuren einbauen kann.DE-A-2 335 570 describes that when using glycols or glycol monoalkyl ethers it is possible to react them with bis-triazinylamino-stilbene-2,2'-disulfonic acid derivatives in the third stage, ie with a Cyanuric chloride derivative that only has one chlorine atom on each triazine ring. However, the yield of this procedure is only between 50 and 80% and therefore makes the procedure unattractive. There was therefore a need for exactly one C 1 -C 4 -alkoxy radical per cyanuric chloride unit in the bis-triazinylamino-stilbene-2,2'-disulfonic acids by a process by means of which one could selectively and with improved yields without the use of complex and expensive reagents can install.

Gemäß US-A-3.951.965 werden Bis-Triazinylamino-stilbendisulfonsäurederivate beschrieben, die durch jeweils stöchiometrische Umsetzung der entsprechenden Edukte erhalten werden. Eine derartige Verfahrensweise hat aber Nachteile hinsichtlich Produktqualität und -Ausbeute. According to US-A-3,951,965 bis-triazinylamino-stilbenedisulfonic acid derivatives described, each by stoichiometric implementation of the corresponding starting materials be preserved. However, such a procedure has disadvantages Product quality and yield.

Es wurde nun ein Verfahren zur Herstellung von bis-alkoxy-triazinyl-aminohaltigen Stilben-disulfonsäuren oder deren Derivaten gefunden, bei dem man bis-chlor-triazinyl-aminohaltige Stilben-disulfonsäuren mit einem C1-C4-Monoalkanol umsetzt, dadurch gekennzeichnet, daß auf 1 Mol der Bis-chlor-triazinyl-aminohaltigen Stilben-disulfonsäure oder deren Derivate wenigstens 10 Mol C1-C4-Monoalkanol eingesetzt werden und das C1-C4-Monoalkanol zusammen mit Wasser eingesetzt wird, wobei der Wassergehalt der Reaktionsmischung vorzugsweise 10-80 Gew.-%, vorzugsweise 25-60 Gew.-%, bezogen auf die Reaktionsmischung, beträgt.A process has now been found for producing bis-alkoxy-triazinyl-amino-containing stilbene disulfonic acids or their derivatives, in which bis-chloro-triazinyl-amino-containing stilbene disulfonic acids are reacted with a C 1 -C 4 -monoalkanol, characterized in that that at least 10 moles of C 1 -C 4 -monoalkanol are used per 1 mole of bis-chloro-triazinyl-amino-containing stilbene-disulfonic acid or its derivatives and the C 1 -C 4 -monoalkanol is used together with water, the water content of the reaction mixture preferably 10-80% by weight, preferably 25-60% by weight, based on the reaction mixture.

In einer bevorzugten Ausführungsform werden auf 1 Mol einer bis-chlor-triazinyl- aminohaltigen Stilben-disulfonsäure bzw. deren Derivate wenigstens 20 Mol des C1-C4-Monoalkanols eingesetzt. Besonders bevorzugt werden 50-500 Mol, insbesondere 100-300 Mol C1-C4-Monoalkanol pro Mol der Bis-chlor-triazinyl-aminohaltigen Stilben-sulfonsäureverbindung eingesetzt.In a preferred embodiment, at least 20 moles of the C 1 -C 4 -monoalkanol are used for 1 mole of a bis-chloro-triazinyl-amino-containing stilbene disulfonic acid or its derivatives. 50-500 moles, in particular 100-300 moles of C 1 -C 4 -monoalkanol per mole of the bis-chloro-triazinyl-amino-containing stilbene sulfonic acid compound are particularly preferably used.

Als bevorzugte C1-C4-Monoalkanole werden Methanol, Ethanol, Isopropanol, n-Propanol, n-Butanol, sek.-Butanol oder tert.-Butanol, insbesondere Methanol eingesetztThe preferred C 1 -C 4 monoalkanols are methanol, ethanol, isopropanol, n-propanol, n-butanol, sec-butanol or tert-butanol, in particular methanol

Besonders bevorzugt ist das Verfahren zur Herstellung von 4,4'-Bis[6-alkoxy-1,3,5-triazin-2-yl-amino]stilben-2,2'-disulfonsäure oder deren Derivate, deren Triazinylreste jeweils in 4-Position mit Aminresten substituiert sind.The process for the preparation of 4,4'-bis [6-alkoxy-1,3,5-triazin-2-yl-amino] stilbene-2,2'-disulfonic acid is particularly preferred or their derivatives, their triazinyl residues are each substituted in the 4-position with amine residues.

Das erfindungsgemäße Verfahren wird vorzugsweise in Gegenwart eines säurebindenden Mittels durchgeführt, wobei als säurebindendes Mittel vorzugsweise Alkalihydroxid, insbesondere Kalium- oder Natriumhydroxid verwendet wird. Das säurebindende Mittel wird vorzugsweise in einer Menge von 2 bis 6 Mol Äquivalenten pro Mol der bis-chlor-triazinyl-aminohaltigen Stilben-disulfonsäure oder deren Derivate eingesetzt, vorzugsweise in einer Menge von 3 bis 4 Mol Äquivalenten.The process according to the invention is preferably carried out in the presence of an acid-binding Carried out, preferably as the acid-binding agent Alkali hydroxide, especially potassium or sodium hydroxide is used. The Acid-binding agent is preferably used in an amount of 2 to 6 mol equivalents per mole of the bis-chloro-triazinyl-amino-containing stilbene disulfonic acid or its Derivatives used, preferably in an amount of 3 to 4 mol equivalents.

Das erfindungsgemäße Verfahren wird in der Regel bei Temperaturen von 0°C bis zum Siedepunkt des Reaktionsgemisches, vorzugsweise bei 15 bis 80°C durchgeführt. In einer bevorzugten Ausführungsform des erfindungsgemäßen Verfahrens werden Verbindungen der allgemeinen Formel (I)

Figure 00040001
hergestellt, worin

M
für Wasserstoff, ein Alkalimetallion oder für ein gegebenenfalls substituiertes Ammoniumion steht,
R1 und R2
unabhängig voneinander C1-C4-Alkyl bedeuten und
R3 und R4
unabhängig voneinander für einen Aminrest stehen.
The process according to the invention is generally carried out at temperatures from 0 ° C. to the boiling point of the reaction mixture, preferably at 15 ° to 80 ° C. In a preferred embodiment of the process according to the invention, compounds of the general formula (I)
Figure 00040001
manufactured in which
M
represents hydrogen, an alkali metal ion or an optionally substituted ammonium ion,
R 1 and R 2
are independently C 1 -C 4 alkyl and
R 3 and R 4
independently represent an amine residue.

Die bevorzugten nach dem erfindungsgemäßen Verfahren hergestellten Verbindungen der Formel (I) werden durch Umsetzung von Verbindungen der Formel (II)

Figure 00040002
worin

R3, R4
und M die oben genannten Bedeutungen haben,
mit C1-C4-Monoalkanolen erhalten.The preferred compounds of the formula (I) prepared by the process according to the invention are obtained by reacting compounds of the formula (II)
Figure 00040002
wherein
R 3 , R 4
and M have the meanings given above,
obtained with C 1 -C 4 monoalkanols.

Verbindungen der Formel (II) werden beispielsweise durch Umsetzung von 2 Äquivalenten Cyanurchlorid mit einem Äquivalent einer Verbindung der Formel (III)

Figure 00050001
und in Summe von 2 Äquivalenten der Verbindungen R3H und R4H in beliebiger Reihenfolge erhalten.Compounds of the formula (II) are obtained, for example, by reacting 2 equivalents of cyanuric chloride with one equivalent of a compound of the formula (III)
Figure 00050001
and obtained in total of 2 equivalents of the compounds R 3 H and R 4 H in any order.

Bevorzugt ist das erfindungsgemäße Verfahren, in dem die Verbindungen der Formel (II) nach ihrer Herstellung nicht zwischenisoliert werden. Besonders bevorzugt ist dabei die Verbindung der Formel (II) in Form ihrer wäßrigen Reaktionslösung, gegebenenfalls nach Aufkonzentrierung und gegebenenfalls (Teil)-Entsalzung in das erfindungsgemäße Herstellungsverfahren einzusetzen.Preferred is the inventive method in which the compounds of Formula (II) can not be isolated between their preparation. Particularly preferred is the compound of formula (II) in the form of its aqueous reaction solution, if necessary after concentration and if necessary (partial) desalination to use in the manufacturing process according to the invention.

In einer weiteren bevorzugten Ausführungsform des erfindungsgemäßen Verfahrens, werden die Verbindungen der Formel (I) ausgehend von einer Verbindung der Formel (II) erhalten, worin R3 und R4 unabhängig voneinander für NR5R6 stehen, wobei R5 für Wasserstoff oder gegebenenfalls substituiertes C1-C6-Alkyl steht und R6 die unter R5 genannten Bedeutungen annehmen kann oder gegebenenfalls substituiertes C5-C8-Cycloalkyl oder gegebenenfalls substituiertes C6-C10-Aryl bedeutet, oder NR5R6 für gegebenenfalls durch C1-C4-Alkyl, insbesondere Methyl substituiertes Morpholino, Piperidino oder Hexamethylenimino stehtIn a further preferred embodiment of the process according to the invention, the compounds of the formula (I) are obtained starting from a compound of the formula (II) in which R 3 and R 4 independently of one another are NR 5 R 6 , where R 5 is hydrogen or optionally substituted C 1 -C 6 alkyl and R 6 can have the meanings given under R 5 or optionally substituted C 5 -C 8 cycloalkyl or optionally substituted C 6 -C 10 aryl, or NR 5 R 6 for optionally by C 1 -C 4 alkyl, in particular methyl-substituted morpholino, piperidino or hexamethyleneimino

Bevorzugte Substituenten des C1-C6-Alkylrestes in der Bedeutung von R5 und R6 sind beispielsweise Hydroxy, C1-C6-Alkoxy, mit C2-C8-Alkoxy substituiertes C2-C8-Alkoxy, C1-C6-Alkylamino oder C1-C6-Dialkylamino, Cyano oder Sulfonsäure bzw. Sulfonat.Preferred substituents of the C 1 -C 6 -alkyl radical in the meaning of R 5 and R 6 are, for example, hydroxyl, C 1 -C 6 -alkoxy, C 2 -C 8 -alkoxy-substituted C 2 -C 8 -alkoxy, C 1 -C 6 alkylamino or C 1 -C 6 dialkylamino, cyano or sulfonic acid or sulfonate.

Als bevorzugte Substituenten des C5-C8-Cycloalkyls kommen in Frage: Halogen, insbesondere Fluor, Chlor und Brom, C1-C6-Alkyl, C1-C6-Alkoxy, Sulfamoyl oder Sulfonyl insbesondere C1-C4-Alkyl.Preferred substituents for C 5 -C 8 cycloalkyl are: halogen, in particular fluorine, chlorine and bromine, C 1 -C 6 alkyl, C 1 -C 6 alkoxy, sulfamoyl or sulfonyl, in particular C 1 -C 4 - Alkyl.

Als gegebenenfalls substituiertes C6-C10-Aryl kommt insbesondere sulfosubstituiertes Phenyl in Frage. Sulfo-substituted phenyl is particularly suitable as an optionally substituted C 6 -C 10 aryl.

Ganz besonders bevorzugt steht R5 für Wasserstoff, Methyl, Sulfoethyl bzw. deren Alkalisalz oder Hydroxyethyl und R6 für Sulfoethyl bzw. deren Alkalisalz, Hydroxyethyl oder disulfosubstituiertes Phenyl.R 5 very particularly preferably represents hydrogen, methyl, sulfoethyl or its alkali salt or hydroxyethyl and R 6 represents sulfoethyl or its alkali salt, hydroxyethyl or disulfo-substituted phenyl.

In einer besonders bevorzugten Ausführungsform sind die Reste R3, R4 sowie R1 und R2 identisch.In a particularly preferred embodiment, the radicals R 3 , R 4 and R 1 and R 2 are identical.

Der Rest M der vorzugsweise für Wasserstoff oder ein Alkalimetall wie Natrium, Kalium oder Lithium steht, muß nicht an jeder im Molekül befindlichen Sulfonsäuregruppe identisch sein.The radical M which is preferably hydrogen or an alkali metal such as sodium, Potassium or lithium does not have to be on every sulfonic acid group in the molecule be identical.

Weiterhin bevorzugt ist es, die nach dem erfindungsgemäßen Verfahren erhältliche Reaktionsmischung zwecks Aufarbeitung auf einen pH von kleiner als 10, vorzugsweise kleiner als 8 einzustellen, und das überschüssige C1-C4-Monoalkanol, vorzugsweise destillativ zu entfernen.It is further preferred to adjust the reaction mixture obtainable by the process according to the invention to a pH of less than 10, preferably less than 8, and to remove the excess C 1 -C 4 -monoalkanol, preferably by distillation.

Die Erfindung betrifft weiterhin Verbindungen der Formel (I), die der Formel (IV) entsprechen,

Figure 00060001
worin

M
die oben angegebene Bedeutung besitzt.
The invention further relates to compounds of the formula (I) which correspond to the formula (IV)
Figure 00060001
wherein
M
has the meaning given above.

Bevorzugte Verbindungen der Formel (IV) sind solche, in denen die SO3M-Gruppen des terminalen Benzolringes in 2- und 5-Position stehen.Preferred compounds of the formula (IV) are those in which the SO 3 M groups of the terminal benzene ring are in the 2- and 5-positions.

Die Verbindungen der Formel (IV) können analog der oben beschriebenen Verfahrensweise hergestellt werden. The compounds of formula (IV) can be analogous to the procedure described above getting produced.

Die nach dem erfindungsgemäßen Verfahren hergestellten Verbindungen (I) sowie die neuen Verbindungen der Formel (IV) eignen sich hervorragend als optische Aufheller für organische Materialien, vorzugsweise für Cellulose, Polyamid, Wolle, Seide und Papier, insbesondere für Photopapier. Sie können auch Waschmitteln zugesetzt werden. Die Verbindungen der Formel (I) können z.B. in Masse eingearbeitet oder auf die Oberfläche der aufzuhellenden Materialien aufgebracht werden. Besonders bevorzugte Einsatzmengen betragen 0,0001 bis 2 Gew.-%, bezogen auf aufzuhellendes Material.The compounds (I) prepared by the process according to the invention and the new compounds of the formula (IV) are outstandingly suitable as optical brighteners for organic materials, preferably for cellulose, polyamide, wool, silk and Paper, in particular for photographic paper. They can also be added to detergents. The compounds of formula (I) can e.g. incorporated in bulk or on the Surface of the materials to be lightened are applied. Particularly preferred The amounts used are 0.0001 to 2% by weight, based on the material to be lightened.

Die in den nachfolgenden Beispielen angegebenen Prozentangaben sind jeweils Gewichtsprozente. The percentages given in the examples below are each Percentages by weight.

Beispiel 1example 1

1 000 g Methanol, welches 10% Wasser enthält, werden vorgelegt. Dann werden 185 g Natronlauge 10%ig zugesetzt. Die Temperatur wird auf 35°C eingestellt. Dann wird innerhalb 1h bei 35°C eine ca. 35°C wanne Lösung aus 167 g 4,4'-Bis[(4-(2,5-disulfo)anilino-6-chloro-1,3,5-triazin-2-yl)amino]-stilben-2,2'-disulfonsäurehexanatriumsalz in 1275 ml Wasser eingetropft. Man hält die Temperatur 2h.1,000 g of methanol, which contains 10% water, are presented. Then be 185 g sodium hydroxide solution 10% added. The temperature is set to 35 ° C. Then a solution of 167 g of 4,4'-bis [(4- (2,5-disulfo) anilino-6-chloro-1,3,5-triazine) solution of 167 g of 4,4'-bis [1 2-yl) amino] -stilbene-2,2'-disulfonic acid hexasodium salt dropped in 1275 ml of water. The temperature is kept for 2 hours.

Der pH wird direkt nach der Umsetzung in ca. 1h durch Zugabe von Salzsäure 10%ig auf 6,5 bis 7,0 gestellt. Danach wird solange Methanol bzw. Methanol-Wasser abdestilliert, bis ein konstanter Siedepunkt von 100°C erreicht ist. Der Ansatz wird bei ca. 30°C mit Wasser auf 1500ml aufgefüllt.
Anschließend wird die Lösung zuerst über ein Blaubandfilter und dann über einen 0,8 µm-Filter abgesaugt, um die Lösung von sämtlichen den Permeatfluß behindernden Trüb- und Schwebstoffen zu befreien. In einer Druckpermeationsanlage werden die 1500 ml eingefüllt. Bei 40 bis 50°C und ca. 40 bar werden die ersten 500 ml Permeat entzogen. Man setzt 500 ml Wasser zu und entzieht die zweiten ca. 500 ml Permeat. Es werden 500 ml Wasser zugesetzt und die dritten ca. 500 ml Permeat entzogen. Es werden 500 ml Wasser zugesetzt und die vierten ca. 500 ml Permeat entzogen. Das Konzentrat wird in einer Kristallisierschale im Vakuumtrockenschrank (50°C) zur Trockenen eingedampft und in einer Reibschale zerkleinert.
The pH is adjusted to 6.5 to 7.0 in about 1 hour by adding 10% hydrochloric acid. Then methanol or methanol-water is distilled off until a constant boiling point of 100 ° C. is reached. The mixture is made up to 1500ml with water at approx. 30 ° C.
The solution is then suctioned off first through a blue-band filter and then through a 0.8 μm filter in order to free the solution from all turbidity and suspended matter which impede the permeate flow. The 1500 ml are filled into a pressure permeation system. The first 500 ml of permeate are removed at 40 to 50 ° C and approx. 40 bar. 500 ml of water are added and the second approx. 500 ml of permeate are removed. 500 ml of water are added and the third approximately 500 ml of permeate are removed. 500 ml of water are added and the fourth approximately 500 ml of permeate are removed. The concentrate is evaporated to dryness in a crystallizing dish in a vacuum drying cabinet (50 ° C.) and comminuted in a friction dish.

Ausbeute: 160 g gelbes Pulver 4,4'-Bis[(4-(2,5-disulfo)anilino-6-methoxy-1,3,5-triazin-2-yl)amino]-stilben-2,2'-disulfonsäurehexanatriumsalz.Yield: 160 g of yellow powder 4,4'-bis [(4- (2,5-disulfo) anilino-6-methoxy-1,3,5-triazin-2-yl) amino] -stilbene-2,2 ' -disulfonic acid hexasodium salt.

Das Produkt enthält weniger als 2 % NaCl und ca. 1 % H2O, so daß sich eine Ausbeute der Theorie von ca. 94 % ergibt.The product contains less than 2% NaCl and approx. 1% H 2 O, so that the theoretical yield is approx. 94%.

Beispiel 2Example 2

1 000 g Methanol, welches 5% Wasser enthält, werden vorgelegt. Dann werden 185 g Natronlauge 10%ig zugesetzt. Die Temperatur wird auf 40°C eingestellt. Dann werden innerhalb 1h bei 40°C 1 200 ml einer wäßrigen Lösung eingetragen, die ca. 65 g 4-[(4-Diethanolamino-6-chloro-1,3,5-triazin-2-yl)amino)4'-[(4-sulfoethylamino-6-chloro-1,3,5-triazin-2-yl)amino]stilben-2,2'-disulfonsäure-trinatriumsalz, 15 g 4,4'-Bis[(4-diethanolamino-6-chloro-1,3,5-triazin-2-yl)amino]stilben-2,2'-disulfonsäure-dinatriumsalz und 65 g 4,4'-Bis[(4-sulfoethylamino-6-chloro-1,3,5-triazin-2-yl)amino]stilben-2,2'-disulfonsäure-tetranatriumsalz enthält. Man hält die Temperatur 2h.1,000 g of methanol, which contains 5% water, are presented. Then be 185 g sodium hydroxide solution 10% added. The temperature is set to 40 ° C. Then 1,200 ml of an aqueous solution are introduced at 40 ° C. within 1 hour, the approx. 65 g of 4 - [(4-diethanolamino-6-chloro-1,3,5-triazin-2-yl) amino) 4 '- [(4-sulfoethylamino-6-chloro-1,3,5- triazin-2-yl) amino] stilbene-2,2'-disulfonic acid trisodium salt, 15 g of 4,4'-bis [(4-diethanolamino-6-chloro-1,3,5-triazin-2-yl) amino] stilbene-2,2'-disulfonic acid disodium salt and 65 g of 4,4'-bis [(4-sulfoethylamino-6-chloro-1,3,5-triazin-2-yl) amino] stilbene-2,2'-disulfonic acid tetrasodium salt contains. The temperature is kept for 2 hours.

Der pH wird direkt nach der Umsetzung in ca. 1h durch Zugabe von Salzsäure 10%ig auf 6,5 bis 7,0 gestellt. Danach wird solange Methanol bzw. Methanol-Wasser abdestilliert, bis ein konstanter Siedepunkt von 100°C erreicht. ist. Der Ansatz wird bei ca. 40 bis 50°C mit Wasser auf 1 800 ml aufgefüllt Anschließend wird die Lösung zuerst über ein Blaubandfilter und dann über einen 0,8 µm-Filter abgesaugt, um die Lösung von sämtlichen den Permeatfluß behindernden Trüb- und Schwebstoffen zu befreien. In einer Druckpermeationsanlage werden die 1 800 ml eingefüllt Bei 40 bis 50°C und ca. 40 bar werden die ersten 600 ml Permeat entzogen. Man setzt 600 ml Wasser zu und entzieht die zweiten ca. 600 ml Permeat. Es werden 600 ml Wasser zugesetzt und die dritten ca. 600 ml Permeat entzogen. Es werden 600 ml Wasser zugesetzt und die vierten ca. 600 ml Permeat entzogen. Das Konzentrat wird in einer Kristallisierschale im Vakuumtrockenschrank (50°C) zur Trockenen eingedampft und in einer Reibschale zerkleinert.
Ausbeute: 140 g hellgelbes Pulver.
The pH is adjusted to 6.5 to 7.0 in about 1 hour by adding 10% hydrochloric acid. Then methanol or methanol-water is distilled off until a constant boiling point of 100 ° C. is reached. is. The mixture is made up to 1,800 ml with water at approx. 40 to 50 ° C. The solution is then suctioned off first through a blue band filter and then through a 0.8 μm filter in order to remove all turbidity and suspended matter which impede the permeate flow to free. The 1,800 ml are filled in a pressure permeation system at 40 to 50 ° C and approx. 40 bar, the first 600 ml permeate are removed. 600 ml of water are added and the second approximately 600 ml of permeate are removed. 600 ml of water are added and the third approximately 600 ml of permeate are removed. 600 ml of water are added and the fourth approximately 600 ml of permeate are removed. The concentrate is evaporated to dryness in a crystallizing dish in a vacuum drying cabinet (50 ° C.) and comminuted in a friction dish.
Yield: 140 g of light yellow powder.

Das Produkt enthält weniger als 1 % NaCl und weniger als 1% Wasser, so daß sich eine Ausbeute der Theorie von 95 % ergibtThe product contains less than 1% NaCl and less than 1% water, so that the theoretical yield is 95%

Beispiel 3Example 3

1 000 g Methanol, welches 5% Wasser enthält, werden vorgelegt. Dann werden 185 g Natronlauge 10%ig zugesetzt. Die Temperatur wird auf 45°C eingestellt. Dann werden innerhalb 1h bei 45°C 600 ml wäßrige 45°C-warme Lösung eingetragen, die ca. 65 g 4-[(4-Diethanolamino-6-chloro-1,3,5-triazin-2-yl)amino]-4'-[(4-sulfoethylamino-6-chloro-1,3,5-triazin-2-yl)amino]stilben-2,2'-disulfonsäure-trinatriumsalz, 15 g 4,4'-Bis[(4-diethanolamino-6-chloro-1,3,5-triazin-2-yl)amino]stilben-2,2'-disulfonsäure-dinatriumsalz und 65 g 4,4'-Bis[(4-sulfoethylamino-6-chloro-1,3,5-triazin-2-yl)amino]stilben-2,2'-disulfonsäure-tetranatriumsalz enthält. Man hält die Temperatur 2h. 1,000 g of methanol, which contains 5% water, are presented. Then be 185 g sodium hydroxide solution 10% added. The temperature is set to 45 ° C. Then 600 ml of aqueous 45 ° C. warm solution are introduced at 45 ° C. within 1 hour, the approx. 65 g of 4 - [(4-diethanolamino-6-chloro-1,3,5-triazin-2-yl) amino] -4 '- [(4-sulfoethylamino-6-chloro-1,3,5 -triazin-2-yl) amino] stilbene-2,2'-disulfonic acid trisodium salt, 15 g of 4,4'-bis [(4-diethanolamino-6-chloro-1,3,5-triazin-2-yl) amino] stilbene-2,2'-disulfonic acid disodium salt and 65 g of 4,4'-bis [(4-sulfoethylamino-6-chloro-1,3,5-triazin-2-yl) amino] stilbene-2,2'-disulfonic acid tetrasodium salt contains. The temperature is kept for 2 hours.

Der pH wird direkt nach der Umsetzung in ca. 1h durch Zugabe von Salzsäure 10%ig auf 6,5 bis 7,0 gestellt. Danach wird solange Methanol bzw. Methanol-Wasser abdestilliert, bis ein konstanter Siedepunkt von 100°C erreicht ist Der Ansatz wird bei ca. 50°C mit Wasser auf 1 200 ml aufgefüllt. Anschließend wird die Lösung zuerst über ein Blaubandfilter und dann über einen 0,8 µm-Filter abgesaugt, um die Lösung von sämtlichen den Permeatfluß behindernden Trüb- und Schwebstoffen zu befreien. In einer Druckpermeationsanlage werden die 1 200 ml eingefüllt. Bei ca. 50°C und ca. 40 bar werden die ersten 400 ml Permeat entzogen. Man setzt 400 ml Wasser zu und entzieht die zweiten ca. 400 ml Permeat Es werden 400 ml Wasser zugesetzt und die dritten ca. 400 ml Permeat entzogen. Es werden 400 ml Wasser zugesetzt und die vierten ca. 400 ml Permeat entzogen. Das Konzentrat wird in einer Kristallisierschale im Vakuumtrockenschrank (50°C) zur Trockenen eingedampft und in einer Reibschale zerkleinert.
Ausbeute: 140 g gelbes Pulver.
The pH is adjusted to 6.5 to 7.0 in about 1 hour by adding 10% hydrochloric acid. Then methanol or methanol-water is distilled off until a constant boiling point of 100 ° C. is reached. The batch is made up to 1200 ml with water at approx. 50 ° C. The solution is then suctioned off first through a blue-band filter and then through a 0.8 μm filter in order to free the solution from all turbidity and suspended matter which impede the permeate flow. The 1,200 ml are filled into a pressure permeation system. The first 400 ml of permeate are removed at approx. 50 ° C and approx. 40 bar. 400 ml of water are added and the second approximately 400 ml of permeate are removed. 400 ml of water are added and the third approximately 400 ml of permeate are removed. 400 ml of water are added and the fourth approximately 400 ml of permeate are removed. The concentrate is evaporated to dryness in a crystallizing dish in a vacuum drying cabinet (50 ° C.) and comminuted in a friction dish.
Yield: 140 g of yellow powder.

Das Produkt enthält weniger als 1 % NaCl und weniger als 1 % Wasser, so daß sich eine Ausbeute der Theorie von 95 % ergibt.The product contains less than 1% NaCl and less than 1% water, so that the theoretical yield is 95%.

Beispiel 4Example 4

1 000 g Ethanol, welches 10% Wasser enthält, werden vorgelegt Dann werden 185 g Natronlauge 10%ig zugesetzt. Die Temperatur wird auf 45°C eingestellt Dann wird innerhalb 1h bei 45°C eine ca. 45°C warme Lösung aus 167 g 4,4'-Bis[(4-(2,5-disulfo)anilino-6-chloro-1,3,5-triazin-2-yl)amino]-stilben-2,2'-disulfonsäurehexanatriumsalz in 1 275 ml Wasser eingetropft. Man hält die Temperatur 4h.1,000 g of ethanol, which contains 10% of water, are initially introduced 185 g sodium hydroxide solution 10% added. The temperature is set to 45 ° C A solution of 167 g of 4,4'-bis [(4- (2,5-disulfo) anilino-6-chloro-1,3,5-triazine) at about 45 ° C. is then heated at 45 ° C. within 1 hour. 2-yl) amino] -stilbene-2,2'-disulfonic acid hexasodium salt dropped in 1 275 ml of water. The temperature is kept for 4 hours.

Der pH wird direkt nach der Umsetzung in ca. 1h durch Zugabe von Salzsäure 10%ig auf 6,5 bis 7,0 gestellt. Danach wird solange Ethanol bzw. Ethanol-Wasser abdestilliert, bis ein konstanter Siedepunkt von 100°C erreicht ist. Der Ansatz wird bei ca. 50°C mit Wasser auf 1500 ml aufgefüllt
Anschließend wird die Lösung zuerst über ein Blaubandfilter und dann über einen 0,8 µm-Filter abgesaugt, um die Lösung von sämtlichen den Permeatfluß behindernden Trüb- und Schwebstoffen zu befreien. In einer Druckpermeationsanlage werden die 1 500 ml eingefüllt. Bei 40 bis 50°C und ca. 40 bar werden die ersten 500 ml Permeat entzogen. Man setzt 500 ml Wasser zu und entzieht die zweiten ca. 500 ml Permeat. Es werden 500 ml Wasser zugesetzt und die dritten ca. 500 ml Permeat entzogen. Es werden 500 ml Wasser zugesetzt und die vierten ca. 500 ml Permeat entzogen.
Das Konzentrat wird in einer Kristallisierschale im Vakuumtrockenschrank (50°C) zur Trockenen eingedampft und in einer Reibschale zerkleinert.
Ausbeute: 165 g gelbes Pulver 4,4'-Bis[(4-(2,5disulfo)anilino-6-ethoxy-1,3,5-triazin-2-yl)amino]-stilben-2,2'-disulfonsäurehexanatriumsalz.
The pH is adjusted to 6.5 to 7.0 in about 1 hour by adding 10% hydrochloric acid. Thereafter, ethanol or ethanol-water is distilled off until a constant boiling point of 100 ° C. is reached. The mixture is made up to 1500 ml with water at approx. 50 ° C
The solution is then suctioned off first through a blue-band filter and then through a 0.8 μm filter in order to free the solution from all turbidity and suspended matter which impede the permeate flow. The 1,500 ml are filled into a pressure permeation system. The first 500 ml of permeate are removed at 40 to 50 ° C and approx. 40 bar. 500 ml of water are added and the second approx. 500 ml of permeate are removed. 500 ml of water are added and the third approximately 500 ml of permeate are removed. 500 ml of water are added and the fourth approximately 500 ml of permeate are removed.
The concentrate is evaporated to dryness in a crystallizing dish in a vacuum drying cabinet (50 ° C.) and comminuted in a friction dish.
Yield: 165 g of yellow powder 4,4'-bis [(4- (2,5 disulfo) anilino-6-ethoxy-1,3,5-triazin-2-yl) amino] -stilbene-2,2'-disulfonic acid hexasodium salt .

Das Produkt enthält weniger als 2 % NaCl und weniger als 2 % Wasser, so daß sich eine Ausbeute der Theorie von 93 % ergibt.The product contains less than 2% NaCl and less than 2% water, so that the theoretical yield is 93%.

Beispiel 5Example 5

425 g Methanol und 75 ml Wasser werden vorgelegt. Dann werden 18 g Natronlauge 45%ig zugesetzt. Dann werden 83 g 4,4'-Bis(2-anilino-6-chloro-1,3,5triazin-2-yl)amino]-stilben-2,2'-disulfonsäure-dinatriumsalz mit einem Wassergehalt von 40% eingetragen. Man erwärmt zum RF. Nach 1h RF setzt man bei ca. 70°C 10 ml gesättigte Natriumchloridlösung zu, läßt auf RT kommen, saugt ab, wäscht mit 160 g Methanol nach und trocknet bei 50°C im Vakuum.
Ausbeute: 49 g gelbes Produkt 4,4'-Bis(2-anilino-6-methoxy-1,3,5-triazin-2-yl)amino]-stilben-2,2'-disulfonsäure-dinatriumsalz, entsprechend 99,5 % der Theorie.
425 g of methanol and 75 ml of water are presented. Then 18 g 45% sodium hydroxide solution are added. Then 83 g of 4,4'-bis (2-anilino-6-chloro-1,3,5-triazin-2-yl) amino] -stilbene-2,2'-disulfonic acid disodium salt with a water content of 40% are added. One heats up to the RF. After 1 h of RF, 10 ml of saturated sodium chloride solution are added at about 70 ° C., the mixture is brought to RT, filtered off with suction, washed with 160 g of methanol and dried at 50 ° C. in vacuo.
Yield: 49 g of yellow product 4,4'-bis (2-anilino-6-methoxy-1,3,5-triazin-2-yl) amino] -stilbene-2,2'-disulfonic acid disodium salt, corresponding to 99. 5% of theory.

Beispiel 6Example 6

800 g Methanol und 350 ml Wasser werden vorgelegt. Dann werden 81 g Natronlauge 10%ig zugesetzt. Dann werden 100 g 4,4'-Bis[(2-(4-sulfo)anilino-6-chloro-1,3,5-triazin-2-yl)amino]-stilben-2,2'-disulfonsäure-tetranatriumsalz mit einem Wassergehalt von 40% eingetragen. Man erwärmt auf 60°C und hält 1h 60°C.
Der pH wird direkt anschließend in ca. 1h durch Zugabe von Salzsäure 10%ig auf 6,5 bis 7,0 gestellt. Danach wird solange Methanol bzw. Methanol-Wasser abdestilliert, bis ein konstanter Siedepunkt von 100°C erreicht ist. Der Ansatz wird bei ca. 50°C mit Wasser auf 500ml aufgefüllt und mit 10%iger Natronlauge auf pH 9,0 gestellt.
800 g of methanol and 350 ml of water are presented. Then 81 g of 10% sodium hydroxide solution are added. Then 100 g of 4,4'-bis [(2- (4-sulfo) anilino-6-chloro-1,3,5-triazin-2-yl) amino] -stilbene-2,2'-disulfonic acid tetrasodium salt registered with a water content of 40%. The mixture is heated to 60 ° C. and kept at 60 ° C. for 1 hour.
The pH is then adjusted to 6.5 to 7.0 in about 1 hour by adding 10% hydrochloric acid. Then methanol or methanol-water is distilled off until a constant boiling point of 100 ° C. is reached. The mixture is made up to 500 ml with water at approx. 50 ° C. and adjusted to pH 9.0 with 10% sodium hydroxide solution.

Anschließend wird die Lösung zuerst über ein Blaubandfilter und dann über einen 0,8 µm-Filter abgesaugt, um die Lösung von sämtlichen den Permeatfluß behindernden Trüb- und Schwebstoffen zu befreien.
In einer Druckpermeationsanlage werden die 500ml eingefüllt. Bei 40 - 50°C und ca. 40 bar werden die ersten 150 ml Permeat entzogen. Man setzt 150 ml Wasser zu und entzieht die zweiten ca. 150 ml Permeat Es werden 150 ml Wasser zugesetzt und die dritten ca. 150 ml Permeat entzogen. Es werden 150 ml Wasser zugesetzt und die vierten ca. 150 ml Permeat entzogen. Das Konzentrat wird in einer Kristallisierschale im Vakuumtrockenschrank (50°C) zur Trockenen eingedampft und in einer Reibschale zerkleinert.
Ausbeute: 56 g gelbes Pulver 4,4'-Bis[(2-(4-sulfo)anilino-6-methoxy-1,3,5-triazin-2-yl)amino]-stilben-2,2'-disulfonsäure-tetranatriumsalz
The solution is then suctioned off first through a blue-band filter and then through a 0.8 μm filter in order to free the solution from all turbidity and suspended matter which impede the permeate flow.
The 500ml are filled in a pressure permeation system. The first 150 ml of permeate are removed at 40 - 50 ° C and approx. 40 bar. 150 ml of water are added and the second approximately 150 ml of permeate are removed. 150 ml of water are added and the third approximately 150 ml of permeate are removed. 150 ml of water are added and the fourth approximately 150 ml of permeate are removed. The concentrate is evaporated to dryness in a crystallizing dish in a vacuum drying cabinet (50 ° C.) and comminuted in a friction dish.
Yield: 56 g of yellow powder 4,4'-bis [(2- (4-sulfo) anilino-6-methoxy-1,3,5-triazin-2-yl) amino] -stilbene-2,2'-disulfonic acid tetrasodium salt

Das Produkt enthält noch 1 % NaCl und 2 % Wasser, so daß sich eine Ausbeute der Theorie von 92 % ergibt.The product still contains 1% NaCl and 2% water, so that there is a yield the theory of 92%.

Claims (9)

  1. Process for the preparation of stilbene-disulphonic acids containing bis-alkoxytriazinyl-amino, or derivatives thereof, characterized in that a stilbene-disulphonic acid containing bis-chloro-triazinyl-amino, or a derivative thereof, is reacted with a C1-C4-monoalkanol, at least 10 mol of C1-C4-monoalkanol being employed per mol of the stilbene-sulphonic acid containing bis-chloro-triazinyl-amino, or derivatives thereof, and the C1-C4-monoalkanol being employed together with water, the water content of the reaction mixture being 10-18% by weight, based on the reaction mixture.
  2. Process according to Claim 1, characterized in that at least 20 mol of C1-C4-monoalkanol are employed per mol of the stilbene-sulphonic acid containing bis-chloro-triazinyl-amino, or derivatives thereof.
  3. Process according to Claim 1, characterized in that methanol is used as the C1-C4-monoalkanol.
  4. Process according to Claim 1, characterized in that the reaction is carried out in the presence of an acid-binding agent, in particular an alkali metal hydroxide.
  5. Process according to Claim 1, characterized in that the stilbene-disulphonic acid containing bis-alkoxy-triazinyl-amino corresponds to the formula (I)
    Figure 00170001
    wherein
    M
    represents hydrogen, an alkali metal ion or an optionally substituted ammonium ion,
    R1 and R2
    independently of one another represent C1-C4-alkyl and
    R3 and R4
    independently of one another represent an amine radical,
    and is prepared starting from compounds of the formula (II)
    Figure 00170002
    wherein R3, R4 and M have the abovementioned meaning.
  6. Compounds of the formula (IV)
    Figure 00180001
    wherein
    M
    represents hydrogen, an alkali metal or optionally substituted ammonium.
  7. Compounds according to Claim 6, characterized in that the two SO3M groups of the terminal benzoring in the formula (IV) are in each case in the 2- and 5-position.
  8. Use of stilbene-disulphonic acids containing bis-alkoxy-triazinyl-amino, or derivatives thereof, according to Claim 6 or 7, for optical brightening of organic materials, in particular of cellulose and paper.
  9. Organic material, in particular cellulose or paper, comprising 0.0001 to 2% by weight of a compound according to Claim 6.
EP96939062A 1995-11-28 1996-11-15 Process for preparing bis-alkoxy-triazinyl-amino-containing stilbene disulphonic acids or their derivatives Expired - Lifetime EP0863884B1 (en)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
DE19544269 1995-11-28
DE19544269A DE19544269A1 (en) 1995-11-28 1995-11-28 Process for the preparation of bis-alkoxy-amino-containing stilbene disulfonic acids or their derivatives
PCT/EP1996/005033 WO1997019937A2 (en) 1995-11-28 1996-11-15 Process for preparing bis-alkoxy-triazinyl-amino-containing stilbene disulphonic acids or their derivatives

Publications (2)

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EP0863884A2 EP0863884A2 (en) 1998-09-16
EP0863884B1 true EP0863884B1 (en) 2001-10-04

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JP (1) JP4115527B2 (en)
CN (1) CN1083441C (en)
BR (1) BR9611766A (en)
DE (2) DE19544269A1 (en)
ES (1) ES2164928T3 (en)
MX (1) MX9804222A (en)
PT (1) PT863884E (en)
WO (1) WO1997019937A2 (en)

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GB0100610D0 (en) * 2001-01-10 2001-02-21 Clariant Int Ltd Improvements in or relating to organic compounds
US8080510B2 (en) * 2006-05-23 2011-12-20 Basf Se Detergent composition for textile fibre materials
US8227808B2 (en) * 2007-12-06 2012-07-24 Chimei Innolux Corporation Method for manufacturing thin film transistor (TFT) and OLED display having TFTS manufactured by the same

Family Cites Families (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2713046A (en) * 1955-07-12 Chachj
DE1444015A1 (en) 1963-08-10 1969-10-09 Bayer Ag Bis-triazinylaminostilbene-disulfonic acid compounds
US3682907A (en) 1968-09-12 1972-08-08 Sumitomo Chemical Co 4,4{40 -bis(2-{62 -sulfoethylamino-4-amino-1,3,5-triazine-6-ylamino)stilbene-2,2{40 -disulfonic
DE2335570A1 (en) * 1972-07-21 1974-01-31 Ciba Geigy Ag Bis-triazinylamino stilbene-2,2'-disulphonic acids prepn - useful as optical brighteners
CH603878B5 (en) * 1973-09-21 1978-08-31 Hoechst Ag
CH647021A5 (en) * 1981-09-22 1984-12-28 Ciba Geigy Ag METHOD FOR PRODUCING STORAGE-STABLE BRIGHTENER FORMULATIONS.
US4866152A (en) * 1988-04-04 1989-09-12 Dow Corning Corporation Aminofunctional organosilicon optical brighteners

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US6248887B1 (en) 2001-06-19
DE19544269A1 (en) 1997-06-05
JP2000502326A (en) 2000-02-29
CN1083441C (en) 2002-04-24
WO1997019937A2 (en) 1997-06-05
WO1997019937A3 (en) 1997-07-24
ES2164928T3 (en) 2002-03-01
PT863884E (en) 2002-03-28
BR9611766A (en) 1999-07-13
MX9804222A (en) 1998-09-30
EP0863884A2 (en) 1998-09-16
CN1202892A (en) 1998-12-23
DE59607845D1 (en) 2001-11-08
JP4115527B2 (en) 2008-07-09

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